CN201161935Y - A lithium bromide absorption air-conditioning seawater desalination system - Google Patents
A lithium bromide absorption air-conditioning seawater desalination system Download PDFInfo
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- CN201161935Y CN201161935Y CNU2007200762250U CN200720076225U CN201161935Y CN 201161935 Y CN201161935 Y CN 201161935Y CN U2007200762250 U CNU2007200762250 U CN U2007200762250U CN 200720076225 U CN200720076225 U CN 200720076225U CN 201161935 Y CN201161935 Y CN 201161935Y
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- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 title claims abstract description 86
- 239000013535 sea water Substances 0.000 title claims abstract description 76
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 33
- 238000004378 air conditioning Methods 0.000 title claims abstract description 33
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000007921 spray Substances 0.000 claims abstract description 17
- 238000001704 evaporation Methods 0.000 claims abstract description 14
- 230000008020 evaporation Effects 0.000 claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 claims abstract description 14
- 239000013505 freshwater Substances 0.000 claims description 8
- 238000005507 spraying Methods 0.000 claims description 4
- 229940059936 lithium bromide Drugs 0.000 claims 14
- 239000006200 vaporizer Substances 0.000 claims 12
- 239000006096 absorbing agent Substances 0.000 abstract description 9
- 230000001105 regulatory effect Effects 0.000 abstract description 5
- 238000000034 method Methods 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 230000004888 barrier function Effects 0.000 description 3
- 230000003749 cleanliness Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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Abstract
一种溴化锂吸收式空调海水淡化系统,包括溴化锂溶液循环产水系统、海水蒸发及空气处理系统。溴化锂溶液循环产水系统:发生冷凝器、热交换器、吸收蒸发器、循环泵、调节阀门组。其中发生冷凝器包括发生器和冷凝器,两者之间连有挡水器。海水蒸发及空气处理系统:吸收蒸发器、海水喷淋室、预热器、调节阀、节流阀、阀门组。其中吸收蒸发器包括吸收器和蒸发器,两者之间连有挡水器。本实用新型可具有空调和海水淡化功能,简化了原先空调系统与海水淡化循环系统的两个单独分离系统,并有效节能。
A lithium bromide absorption air-conditioning seawater desalination system includes a lithium bromide solution circulation water production system, seawater evaporation and air treatment systems. Lithium bromide solution circulating water production system: generating condenser, heat exchanger, absorption evaporator, circulating pump, regulating valve group. Wherein the generating condenser includes a generator and a condenser, and a water retainer is connected between the two. Seawater evaporation and air treatment system: absorption evaporator, seawater spray chamber, preheater, regulating valve, throttle valve, valve group. The absorption evaporator includes an absorber and an evaporator, and a water retainer is connected between the two. The utility model can have the functions of air-conditioning and seawater desalination, which simplifies the two separate separate systems of the original air-conditioning system and seawater desalination circulation system, and effectively saves energy.
Description
技术领域 technical field
本实用新型涉及制冷设备,具体为一种船用的可同时实现空调制冷和海水淡化的系统。The utility model relates to refrigeration equipment, in particular to a marine system capable of realizing air-conditioning refrigeration and seawater desalination at the same time.
背景技术 Background technique
船用热法海水淡化技术要使海水在60℃左右的发动机缸套水温度下蒸发,而海水中含有较多的钙、镁离子,在此温度下很容易结成水垢,因此在现有的热法海水淡化技术中都要对海水进行软化处理,这使得海水淡化的成本增加;而海水淡化的副产品——浓海水未经利用即排放了。事实上,浓海水具有较强的吸湿能力。另一方面,在海洋气候环境下,空调负荷中潜热负荷(湿负荷)所占的比例远大于内陆,而在其他条件相同的情况下,处理潜热负荷比处理显热负荷需要更低的制冷温度,这也使得制冷机能耗增大。Marine thermal seawater desalination technology needs to evaporate seawater at the engine jacket water temperature of about 60°C, and seawater contains more calcium and magnesium ions, which are easy to form scale at this temperature. Seawater desalination technology must soften seawater, which increases the cost of seawater desalination; and the by-product of seawater desalination—concentrated seawater is discharged without being used. In fact, concentrated seawater has a strong ability to absorb moisture. On the other hand, in the marine climate environment, the proportion of latent heat load (humidity load) in the air conditioning load is much larger than that of the inland, and under the same conditions, the processing of the latent heat load requires lower cooling than the processing of the sensible heat load. temperature, which also increases the energy consumption of the refrigerator.
实用新型内容Utility model content
本实用新型所解决的技术问题在于提供一种同时运行空调和海水淡化的系统,主要运用于远洋船舶和海上平台的空调与海水淡化系统。The technical problem solved by the utility model is to provide a system for simultaneously operating air conditioning and seawater desalination, which is mainly used in the air conditioning and seawater desalination systems of ocean-going ships and offshore platforms.
本实用新型所解决的技术问题可以采用以下技术方案来实现:The technical problem solved by the utility model can be realized by adopting the following technical solutions:
一种溴化锂吸收式空调海水淡化系统,包括溴化锂溶液循环产水系统、海水蒸发及空气处理系统,其特征在于:所述溴化锂溶液循环产水系统,包括,发生冷凝器、热交换器、吸收蒸发器、循环泵;所述溴化锂溶液循环产水系统由发生冷凝器通过溴化锂溶液管路连接热交换器,吸收蒸发器通过溴化锂溶液管路连接热交换器和循环泵,所述循环泵通过溴化锂溶液管路连接吸收蒸发器和热交换器组成;所述海水蒸发及空气处理系统,包括,海水喷淋室、吸收蒸发器、预热器;所述海水蒸发及空气处理系统由海水喷淋室通过浓海水管路和风管连接吸收蒸发器,吸收蒸发器通过淡水管路和海水管路连接预热器。A lithium bromide absorption air-conditioning seawater desalination system, including a lithium bromide solution circulating water production system, seawater evaporation and air treatment system, characterized in that: the lithium bromide solution circulating water production system includes a generating condenser, a heat exchanger, an absorption evaporation The lithium bromide solution circulation water production system is connected to the heat exchanger through the lithium bromide solution pipeline by the generation condenser, and the absorption evaporator is connected to the heat exchanger and the circulation pump through the lithium bromide solution pipeline, and the circulation pump is passed through the lithium bromide solution pipeline. The pipeline is connected to an absorption evaporator and a heat exchanger; the seawater evaporation and air treatment system includes a seawater spray room, an absorption evaporator, and a preheater; the seawater evaporation and air treatment system passes through the seawater spray room The concentrated seawater pipeline and the air pipe are connected to the absorption evaporator, and the absorption evaporator is connected to the preheater through the fresh water pipeline and the seawater pipeline.
为达到简化系统的目的,所述溴化锂溶液循环产水系统和海水蒸发及空气处理系统共用一个吸收蒸发器。In order to achieve the purpose of simplifying the system, the lithium bromide solution circulating water production system and the seawater evaporation and air treatment system share an absorption evaporator.
所述吸收蒸发器包括吸收器和蒸发器,吸收器与蒸发器之间连有挡水器。The absorption evaporator includes an absorber and an evaporator, and a water retainer is connected between the absorber and the evaporator.
所述发生冷凝器包括发生器和冷凝器,发生器与冷凝器之间连有挡水器。The generating condenser includes a generator and a condenser, and a water barrier is connected between the generator and the condenser.
所述发生器、吸收器、蒸发器设有喷淋装置。The generator, absorber and evaporator are equipped with spraying devices.
位于吸收器与蒸发器之间的挡水器的主要作用是防止从发生器经换热器流下来的溴化锂浓溶液在吸收器喷淋时溅射到蒸发器,同时保持吸收器与蒸发器之间的水蒸气通道。The main function of the water barrier located between the absorber and the evaporator is to prevent the concentrated lithium bromide solution flowing down from the generator through the heat exchanger from splashing to the evaporator when the absorber is sprayed, while maintaining the distance between the absorber and the evaporator. the water vapor passage between them.
位于发生器与冷凝器之间的挡水器的主要作用是防止从吸收器泵送上来的溴化锂稀溶液在发生器喷淋时溅射到冷凝器,同时保持发生器与冷凝器之间的水蒸气通道。The main function of the water barrier located between the generator and the condenser is to prevent the dilute lithium bromide solution pumped up from the absorber from splashing into the condenser when the generator is sprayed, and at the same time keep the water between the generator and the condenser vapor channel.
所述发生冷凝器连接射流真空泵,目的用于维持整个系统运行所须的真空度。The generating condenser is connected with a jet vacuum pump for maintaining the vacuum required for the operation of the whole system.
这里为了方便区分,所以从功能上把整个一种溴化锂吸收式空调海水淡化系统分为两个循环系统,即溴化锂溶液循环产水系统、海水蒸发及空气处理系统。Here, for the convenience of distinction, functionally, the whole lithium bromide absorption air-conditioning desalination system is divided into two circulation systems, namely lithium bromide solution circulation water production system, seawater evaporation and air treatment system.
一方面,从空调的功能上讲,海水经预热器进入吸收蒸发器的喷淋装置,并喷淋到热管换热管器上,通过蒸发器的热管换热器吸收空气中的热量使海水蒸发、浓缩,分离成水蒸汽和浓海水。水蒸汽通过挡水器被喷淋而下的溴化锂浓溶液吸收。空调新风与回风的混合风送入海水喷淋室。浓海水在海水喷淋室喷淋,同混合风进行热质交换,使空气的温度、适度降低,使其洁净度提高,而浓海水在吸收了混合风的部分热量、水分及污物后排出系统;混合风在吸收蒸发器通过热管换热器,将剩余的空调热负荷传递给海水,使空气的温度、湿度达到送风要求。On the one hand, from the function of the air conditioner, the seawater enters the spray device of the absorption evaporator through the preheater, and sprays onto the heat pipe heat exchanger, and the heat pipe heat exchanger of the evaporator absorbs the heat in the air to make the seawater Evaporate, concentrate, and separate into water vapor and concentrated seawater. The water vapor is absorbed by the concentrated lithium bromide solution sprayed down through the water retainer. The mixed air of air-conditioning fresh air and return air is sent into the seawater spray room. The concentrated seawater is sprayed in the seawater spray room, and exchanges heat and mass with the mixed air, so that the temperature of the air is moderately lowered and the cleanliness is improved, and the concentrated seawater is discharged after absorbing part of the heat, moisture and dirt of the mixed air. System; the mixed wind passes through the heat pipe heat exchanger in the absorption evaporator, and transfers the remaining heat load of the air conditioner to the seawater, so that the temperature and humidity of the air meet the requirements of the air supply.
另一方面,从海水淡化的功能上讲,经过吸收蒸发器喷淋的溴化锂浓溶液吸收了水蒸汽后稀释成稀溶液,并由循环泵输送,经热交换器回收浓溴化锂溶液的热量,升温后,送入发生冷凝器喷淋,被发动机余热加热后,蒸发制成水蒸汽、以及溴化锂浓溶液;水蒸汽通过挡水器经冷却后凝结成淡水,浓溴化锂溶液经热交换器,降温后进入吸收蒸发器喷淋,进入下一个循环。On the other hand, in terms of the function of desalination of seawater, the concentrated lithium bromide solution sprayed by the absorption evaporator absorbs water vapor and is diluted into a dilute solution, which is transported by a circulating pump, and the heat of the concentrated lithium bromide solution is recovered by a heat exchanger to raise the temperature. After that, it is sent to the condenser for spraying. After being heated by the waste heat of the engine, it evaporates to form water vapor and concentrated lithium bromide solution; the water vapor passes through the water retainer and is cooled to condense into fresh water. Enter the absorption evaporator to spray and enter the next cycle.
有益效果:①.海水在温度较低的状况下进行蒸发,可避免在换热管上结垢,简化海水预处理工艺,即海水可不进行软化处理。Beneficial effects: ①. The seawater evaporates at a lower temperature, which can avoid scaling on the heat exchange tubes and simplify the seawater pretreatment process, that is, the seawater does not need to be softened.
②.采用浓海水处理空气,不但使空气得到净化,而且承担了部分空调负荷,使空调的制冷负荷降低,特别是湿负荷的降低。②. The use of concentrated seawater to treat the air not only purifies the air, but also undertakes part of the air conditioning load, reducing the cooling load of the air conditioner, especially the humidity load.
③.由于湿负荷的降低,使空调制冷温度可以提高,从而提高了空调制冷系统的热效率。③. Due to the reduction of the humidity load, the cooling temperature of the air conditioner can be increased, thereby improving the thermal efficiency of the air conditioner refrigeration system.
附图说明 Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式 Detailed ways
为了使本实用新型实现的技术手段、创作特征、达成目的与功效易于明白了解,下面结合具体图示,进一步阐述本实用新型。In order to make the technical means, creative features, goals and effects achieved by the utility model easy to understand, the utility model will be further elaborated below in conjunction with specific illustrations.
一种溴化锂吸收式空调海水淡化系统,包括溴化锂溶液循环产水系统A、海水蒸发及空气处理系统B。A lithium bromide absorption air-conditioning seawater desalination system comprises a lithium bromide solution circulating water production system A, seawater evaporation and air treatment system B.
溴化锂溶液循环产水系统A:发生冷凝器1、热交换器2、吸收蒸发器3、循环泵4、调节阀门组81(阀门811、阀门812)、调节阀门组82(阀门821、阀门822)。其中发生冷凝器1包括发生器11和冷凝器12,两者之间连有挡水器13。Lithium bromide solution circulating water production system A:
海水蒸发及空气处理系统B:吸收蒸发器3、海水喷淋室5、预热器6、调节阀83、节流阀84、阀门组85(阀门851、阀门852)。其中吸收蒸发器3包括吸收器31和蒸发器32,两者之间连有挡水器33。Seawater evaporation and air treatment system B:
本实用新型可分别实现空调和海水淡化功能,每个功能的工作过程如下:The utility model can respectively realize the functions of air conditioning and seawater desalination, and the working process of each function is as follows:
空调功能,海水经预热器6进入吸收蒸发器3的喷淋装置,并喷淋到热管换热管器上,通过蒸发器32的热管换热器吸收空气中的热量使海水蒸发、浓缩,分离成水蒸汽和浓海水。水蒸汽通过挡水器33被喷淋而下的溴化锂浓溶液吸收。空调新风与回风的混合风送入海水喷淋室5。浓海水在海水喷淋室5喷淋,同混合风进行热质交换,使空气的温度、适度降低,使其洁净度提高,而浓海水在吸收了混合风的部分热量、水分及污物后排出系统;混合风在吸收蒸发器3通过热管换热器71,将剩余的空调热负荷传递给海水,使空气的温度、湿度达到送风要求。Air-conditioning function, the seawater enters the spray device of the
海水淡化功能,经过吸收蒸发器3喷淋的溴化锂浓溶液吸收了水蒸汽后稀释成稀溶液,并由循环泵4输送,经热交换器2回收浓溴化锂溶液的热量,升温后,送入发生冷凝器喷淋1,被发动机余热加热后,蒸发制成水蒸汽、以及溴化锂浓溶液;水蒸汽通过挡水器13经冷却后凝结成淡水,浓溴化锂溶液经热交换器2,降温后进入吸收蒸发器3喷淋,进入下一个循环。Seawater desalination function, the concentrated lithium bromide solution sprayed by the
本系统可按照4种工况运行,分别为淡水产量和空调负荷匹配、空调负荷较低、纯制淡水、纯空调制冷。The system can operate according to 4 working conditions, namely fresh water production and air-conditioning load matching, low air-conditioning load, pure fresh water, and pure air-conditioning refrigeration.
工况1:淡水产量和空调负荷相匹配,即空调负荷和海水的蒸发的蒸汽量相匹配。此时,阀门811、阀门821、阀门组85全开,阀门812、阀门822、阀门组83全闭系统工作过程如上所述。Working condition 1: The fresh water output matches the air-conditioning load, that is, the air-conditioning load matches the amount of steam evaporated from seawater. At this time, the
工况2:空调负荷较低。此时,阀门811、阀门组85全开,阀门812、阀门组83全闭,阀门组82适当开启,用部分冷凝热来预热海水,系统工作过程不变。Working condition 2: The air conditioning load is low. At this time,
工况3:纯制淡水。此时,阀门812、阀门822、阀门组85全开,阀门811、阀门821、阀门83全闭,阀门组82适当开启,用部分冷凝热来预热海水,并用吸收热通过热管换热器加热海水。空调风系统停止工作,系统其他工作过程不变。Working condition 3: pure fresh water. At this time,
工况4:纯空调制冷。此时阀门811、阀门821、阀门83全开,阀门812、阀门822、阀门组85全闭,系统按溴化锂吸收式制冷循环运行。Working condition 4: Pure air-conditioning refrigeration. Now
本实用新型可具有空调和海水淡化功能,简化了原先空调系统与海水淡化循环系统的两个单独分离系统,并有效节能。The utility model can have the functions of air conditioning and seawater desalination, which simplifies the two separate separate systems of the original air conditioning system and the seawater desalination circulation system, and effectively saves energy.
以上显示和描述了本实用新型的基本原理和主要特征和本实用新型的优点。本行业的技术人员应该了解,本实用新型不受上述实施例的限制,上述实施例和说明书中描述的只是说明本实用新型的原理,在不脱离本实用新型精神和范围的前提下,本实用新型还会有各种变化和改进,这些变化和改进都落入要求保护的本实用新型范围内。本实用新型要求保护范围由所附的权利要求书及其等效物界定。The basic principles and main features of the present utility model and the advantages of the present utility model have been shown and described above. Those skilled in the art should understand that the utility model is not limited by the above-mentioned embodiments. The above-mentioned embodiments and descriptions only illustrate the principle of the utility model. Without departing from the spirit and scope of the utility model, the utility model The new model also has various changes and improvements, and these changes and improvements all fall within the scope of the claimed utility model. The scope of protection required by the utility model is defined by the appended claims and their equivalents.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101344298B (en) * | 2007-11-15 | 2010-06-09 | 上海海事大学 | Combined operation system of air conditioning and seawater desalination |
| CN102874969A (en) * | 2012-10-15 | 2013-01-16 | 程刚 | Interactive absorption type solar energy and wind energy sea water desalting device |
| CN103073083A (en) * | 2013-01-31 | 2013-05-01 | 东南大学常州研究院 | Air-moistening and solution-moisture-absorption solar fresh water production device and use method thereof |
| CN106237636A (en) * | 2016-08-26 | 2016-12-21 | 创源科瑞环保科技(北京)有限公司 | For separating the system of moisture in feed liquid and applying its method of evaporating |
| CN106277142A (en) * | 2016-09-19 | 2017-01-04 | 武汉大学 | A kind of degree of depth energy conservation sea water desalting apparatus |
| CN109708338A (en) * | 2017-10-25 | 2019-05-03 | 北京华源泰盟节能设备有限公司 | A kind of sewage, seawater vacuum evaporator and absorption heat pump |
-
2007
- 2007-11-15 CN CNU2007200762250U patent/CN201161935Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101344298B (en) * | 2007-11-15 | 2010-06-09 | 上海海事大学 | Combined operation system of air conditioning and seawater desalination |
| CN102874969A (en) * | 2012-10-15 | 2013-01-16 | 程刚 | Interactive absorption type solar energy and wind energy sea water desalting device |
| CN103073083A (en) * | 2013-01-31 | 2013-05-01 | 东南大学常州研究院 | Air-moistening and solution-moisture-absorption solar fresh water production device and use method thereof |
| CN103073083B (en) * | 2013-01-31 | 2014-10-08 | 东南大学常州研究院 | Air-moistening and solution-moisture-absorption solar fresh water production device and use method thereof |
| CN106237636A (en) * | 2016-08-26 | 2016-12-21 | 创源科瑞环保科技(北京)有限公司 | For separating the system of moisture in feed liquid and applying its method of evaporating |
| CN106277142A (en) * | 2016-09-19 | 2017-01-04 | 武汉大学 | A kind of degree of depth energy conservation sea water desalting apparatus |
| CN106277142B (en) * | 2016-09-19 | 2019-06-11 | 武汉大学 | A deep energy-saving seawater desalination device |
| CN109708338A (en) * | 2017-10-25 | 2019-05-03 | 北京华源泰盟节能设备有限公司 | A kind of sewage, seawater vacuum evaporator and absorption heat pump |
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